JPS62193635A - Turbine type stirrer assembly - Google Patents
Turbine type stirrer assemblyInfo
- Publication number
- JPS62193635A JPS62193635A JP62032568A JP3256887A JPS62193635A JP S62193635 A JPS62193635 A JP S62193635A JP 62032568 A JP62032568 A JP 62032568A JP 3256887 A JP3256887 A JP 3256887A JP S62193635 A JPS62193635 A JP S62193635A
- Authority
- JP
- Japan
- Prior art keywords
- blades
- rotor
- liquid
- assembly according
- turbine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000007788 liquid Substances 0.000 claims abstract description 34
- 239000012530 fluid Substances 0.000 claims abstract description 21
- 238000002347 injection Methods 0.000 claims description 11
- 239000007924 injection Substances 0.000 claims description 11
- 230000002776 aggregation Effects 0.000 claims 1
- 238000004220 aggregation Methods 0.000 claims 1
- 230000007704 transition Effects 0.000 claims 1
- 239000006185 dispersion Substances 0.000 abstract description 13
- 230000001154 acute effect Effects 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 description 2
- 241000220317 Rosa Species 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 210000003746 feather Anatomy 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
- B01F23/2331—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
- B01F23/2331—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
- B01F23/23311—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements through a hollow stirrer axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
- B01F23/2331—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
- B01F23/23314—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements through a hollow stirrer element
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
- B01F23/2336—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer
- B01F23/23362—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer the gas being introduced under the stirrer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
- B01F27/1123—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades sickle-shaped, i.e. curved in at least one direction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
- B01F27/1125—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/115—Stirrers characterised by the configuration of the stirrers comprising discs or disc-like elements essentially perpendicular to the stirrer shaft axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/19—Stirrers with two or more mixing elements mounted in sequence on the same axis
- B01F27/192—Stirrers with two or more mixing elements mounted in sequence on the same axis with dissimilar elements
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
- Accessories For Mixers (AREA)
- Liquid Crystal Substances (AREA)
- Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は液体中に流体を分散する攪拌機に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an agitator for dispersing a fluid in a liquid.
多数の軸方向に整合した平坦なかい(櫂)状羽根を備え
た円板型タービン攪拌機がタンク内の液体中に小さい泡
として噴射されたガスを分散してタンクの内容物と混合
することは公知である。使用中、低圧の渦区域がタービ
ンの各回転羽根の背後に、そして工業において屡々遭遇
するガス流量に対して形成され、ガスは集合してこの区
域に空所を形成し易く;このことは不都合なことに分散
および混合の効率を低下しタービン翼を腐食させる。It is known that a disk-type turbine agitator with a large number of axially aligned flat paddle blades disperses the gas injected as small bubbles into the liquid in the tank and mixes it with the contents of the tank. It is. In use, a low-pressure vortex area is formed behind each rotating blade of the turbine and for gas flow rates often encountered in industry, and the gas tends to collect and form cavities in this area; this is disadvantageous. In particular, it reduces dispersion and mixing efficiency and corrodes turbine blades.
同じ問題がタンクの液体より密度の低い噴射された液体
の分散に対しても見出される。本発明者等は渦流の発生
およびその有害な結果を最少比にし、有効な分散および
混合を達成するタービン攪拌機を得た。The same problem is found for the dispersion of injected liquids which are less dense than the tank liquid. The inventors have now achieved a turbine agitator that minimizes the generation of turbulence and its deleterious consequences and achieves effective dispersion and mixing.
したがって、本発明は液体用貯槽、貯槽内に設けられ多
数の半径方向に延びる羽根を有するロータ、および流体
を貯槽内の液体中に噴射する装置を備え、流体噴射装置
およびロータは、使用時、液体中に浸漬したロータ羽根
およびロータ羽根が発生した液体流のいずれか一方また
は双方が噴射された液体を分散するように構成配置され
たタービン式攪拌機集合体であって、各羽根が中空でか
つ不連続な端部、鋭角をなず唯一つの後端部を有し、外
側に凹状面を有せずまた半径方向外端が開放しているこ
とを特徴とする、タービン式攪拌機集合体を提供するも
のである。Accordingly, the present invention comprises a reservoir for a liquid, a rotor disposed within the reservoir and having a number of radially extending vanes, and a device for injecting fluid into the liquid in the reservoir, the fluid ejection device and the rotor, in use. A turbine-type agitator assembly configured and arranged so that one or both of a rotor blade immersed in a liquid and a liquid stream generated by the rotor blade disperses the injected liquid, wherein each blade is hollow and Provided is a turbine-type stirrer assembly, characterized in that it has a single rear end without discontinuous ends, no acute angles, has no concave surface on the outside, and is open at the radially outer end. It is something to do.
通常の円板型タービン式攪拌機においては、渦流は羽根
の表面に沿って流線でないところに発生ずるが、例えば
円形、楕円形、矩形または長円形断面の羽根に関して、
例えば後端面が凹状であるかまたは鋭角的後端が存在し
ない、突出端(例えば通常の軸線方向に整合したかい状
の羽根の軸方向端部)において、分離する。In a typical disk-type turbine agitator, the vortex is generated along the surface of the blade in a non-streamlined area;
Separation occurs, for example, at a protruding end (eg, the axial end of a normally axially aligned paddle blade) where the trailing surface is concave or there is no sharp trailing edge.
本発明の羽根に対しては前記基準を満たすならばいかな
る羽根も適している。この中において、羽根はくさび型
または鋭い長パラボラ型または楕円形断面の後端部にス
ムースに移行する円形、パラボラ形または楕円形断面を
有する対称的断面をもつことができる。“鋭角をなす後
端部”なる語は角度をなす端部ならびに鋭いアールを備
えた端部の両方の意味を有する。パラボラ形または楕円
形断面の先端は、先端部分をくさび形のものとすること
ができるが、羽根の周りの流線を改善するのに好ましい
。好ましい羽根の形は対称的な翼型断面である。Any blade meeting the above criteria is suitable for the blade of the present invention. In this, the vanes can have a symmetrical cross-section with a circular, parabolic or oval cross-section smoothly transitioning to a wedge-shaped or sharply elongated parabolic or oval cross-section at the rear end. The term "acute trailing edge" has the meaning of both an angled edge as well as an edge with a sharp radius. A parabolic or elliptical cross-section tip is preferred to improve flow lines around the vane, although the tip portion can be wedge-shaped. The preferred blade shape is a symmetrical airfoil cross section.
羽根は中空で先端は不連続の、例えば孔の形式の、また
は好ましくは対称的断面の羽根の先端面に対称的に設け
られた溝の形式とされる。The vanes are hollow and have discontinuous tips, for example in the form of holes or in the form of grooves symmetrically provided in the tip surface of the vane, preferably of symmetrical cross-section.
羽根の半径方向外端は少なくとも部分的に開放し、そこ
でそのような羽根はすくい上げ作用を奏しすくい上げた
液体ν半径方向外方に給送することにより分散し混合す
る。The radially outer ends of the vanes are at least partially open, such vanes having a scooping action and dispersing and mixing the scooped liquid v by feeding it radially outward.
本発明集合体の羽根の通常の寸法は:
羽根の長さ−D/4、突出高さ−D15である(ここに
、Dはロータ直径の全長)。Typical dimensions of the blades of the inventive assembly are: blade length - D/4, protrusion height - D15 (where D is the total length of the rotor diameter).
羽根は通常タービン攪拌機のかい用として金属またはプ
ラスチックから作られる。The blades are usually made of metal or plastic for turbine agitator paddles.
羽根は全体的形式において、羽根の平面を限定する、半
径方向および横方向軸の二つの長い軸線、を有する。こ
の羽根の平面は一般に使用中羽根によって描かれるいか
なる回転面に対しても一致するかまたは平行になり、す
なわち羽根は通常ロータ軸にまたはロータ軸に対して“
迎え角”では固定されない。しかしながら、この迎え角
の可能性は除外されないが、角度は後端(または先端)
が軸方向に突出する端部として有効に作用すること、お
よびかなりの渦流を発生ずる傾向があるため羽根の面の
後端部分が凹状面として有効に作用することのいずれか
一方または双方が起こる程に大きくないことは容易に理
解しうろことである。In its general form, the vane has two long axes, a radial and a transverse axis, which define the plane of the vane. The plane of this vane will generally be coincident with or parallel to any plane of rotation described by the vane in use, i.e. the vane will normally be “on” or “with respect to” the rotor axis.
However, the possibility of this angle of attack is not excluded, but the angle is not fixed at the trailing end (or leading end).
may act effectively as an axially projecting end, and/or the rear end portion of the blade surface may act effectively as a concave surface due to its tendency to generate significant vortices. It is easy to understand that it is not that big.
タービンロータの羽根は同じ回転平面内に設けられるか
またはいくつかの回転平面内に設けることができる。羽
根は回転の平衡が最大になるようにいずれか一つの平面
内に規則的に配置されるのが好ましい。好ましくはそれ
らはまた通常の技術的慣行に従って捩り平衡が最大にな
るような(なり易い)軸に沿いかつ別の平面内の各羽根
に対して配置され、例えばそれらは各平面内に同じ数の
羽根を、また対応する数の羽根を異なった平面内に軸方
向に整合してまた相対的に回転方向に規則的にずらして
配置される。The blades of the turbine rotor can be arranged in the same plane of rotation or in several planes of rotation. Preferably, the vanes are regularly arranged in any one plane to maximize rotational balance. Preferably they are also arranged in accordance with normal engineering practice along the axis such that torsional balance is maximized and for each vane in another plane, for example they have the same number of vanes in each plane. The vanes, and a corresponding number of vanes, are arranged in different planes in axial alignment and regularly staggered relative to each other in the direction of rotation.
羽根はまた軸方向にロータ軸に対して、排出流の軸方向
成分を発生するため、直角以外の角度をなして固定する
ことができる。The vanes can also be fixed axially to the rotor axis at an angle other than a right angle to generate an axial component of the exhaust flow.
ロータは2枚以上の羽根をもつことができる。A rotor can have two or more blades.
タービンの混合効率は、羽根が使用中ある羽根の作用が
後続の羽根の作用と干渉するような横方向の寸法に接近
する点まで、一般にどの平面においても羽根の数ととも
に増加する。同様に羽根の平面の有用な数は接近による
平面間の相互の干渉によって制限される。羽槙の一層の
増加は単一の軸方向噴射源から益々遠くなるためタービ
ンの流体分散効率を増大せず、却って貯槽内の液体およ
び液体−流体の一方または双方の分散を助ける。The mixing efficiency of a turbine generally increases with the number of blades in any plane until the blades approach a lateral dimension such that in use the action of one blade interferes with the action of a subsequent blade. Similarly, the useful number of blade planes is limited by mutual interference between the planes due to their proximity. A further increase in the flow rate does not increase the fluid dispersion efficiency of the turbine as it is further away from a single axial injection source, but rather aids in the dispersion of the liquid and/or liquid-fluid within the reservoir.
前記に関連して適当な羽根の数は同一平面では2枚ない
し24枚、通常4枚ないし12枚、また平面数は5まで
通常1である。In connection with the above, the suitable number of blades is 2 to 24, usually 4 to 12 in the same plane, and the number of planes is 5 to 5, usually 1.
通常、ロータの寸法は貯槽の大きさによって決定される
が、通常その直径は対応する貯槽の横方向寸法の1/3
ないし半分である。Typically, the dimensions of the rotor are determined by the size of the reservoir, typically its diameter is 1/3 of the lateral dimension of the corresponding reservoir.
Or half.
流体噴射装置は単一の孔または、列状、格子状ローズ状
またはリング状とすることができる。液体の噴射、とく
に貯槽内の液体より密度の小さい液体も除外されないが
、噴射流体はしばしばガスとされる。The fluid ejector can be a single hole or a row, a lattice, a rose, or a ring. The injection fluid is often a gas, although injection of liquid, especially a liquid with a lower density than the liquid in the reservoir, is not excluded.
ロータおよび流体噴射装置は適当に配置および相互位置
に設けることができるが、それば流体がロータ羽根が掃
過した容積またはロータ羽根によって発生された液体流
が衝突する直ぐ近傍に(両方の場合“分散区域”と称す
る)供給される。The rotor and the fluid injection device may be suitably arranged and positioned relative to each other, provided that the fluid is in the volume swept by the rotor blades or in the immediate vicinity of the impingement of the liquid stream generated by the rotor blades (in both cases “ (referred to as "dispersion area").
ロータはいかなる位置に取付けることもできるが、貯槽
の上または下に取付けられた噴射装置に対して、例えば
それから軸方向に離して、直立して取付けるのが便利で
あり、そこで流体は本質的に重力を受ける液体を通って
分散区域に、ガスまたは貯槽の液体より密度の小さい液
体に対しては下からまた密度の大きい液体に対しては上
から、供給することができる。噴射装置は、ローズ状ま
たはロータに対してリング状の、孔とすることが適当で
ある。Although the rotor can be mounted in any position, it is convenient to mount it upright, for example axially away from the injector mounted above or below the reservoir, where the fluid is essentially It is possible to feed the dispersion zone through the liquid under gravity, from below for liquids with a lower density than the gas or liquid in the reservoir, and from above for liquids with a higher density. The injection device is suitably a hole, rose-shaped or ring-shaped relative to the rotor.
タービン攪拌機に対して通常のように、羽根がロータ軸
自体から延びることは一般的ではなくそれぞれ腕または
軸上の同様の構造物に取付けられる。軸方向の孔、ロー
ズ状またはリング状噴射装置は羽根に重なることのない
ロータの直径より小さい直径を有し、装置は偏向器なし
に分散区域に流体を供給することはない。このような場
合、羽根はロータ円板の外周から延びるように取付ける
のが便利であり、円板は偏向器として作用する。The vanes typically do not extend from the rotor shaft itself, as is usual for turbine agitators, but are each attached to an arm or similar structure on the shaft. The axial hole, rose-shaped or ring-shaped injector has a diameter smaller than the diameter of the rotor without overlapping the blades, and the device does not supply fluid to the dispersion zone without a deflector. In such cases, it is convenient to mount the vanes so that they extend from the outer periphery of the rotor disk, with the disk acting as a deflector.
上記の通常の羽根の寸法に対して、ロータの直径をDと
すると、円板の直径は通常3D/4である。For the above-mentioned normal blade dimensions, if the rotor diameter is D, the disk diameter is usually 3D/4.
流体は勿論羽根が掃過する容積の半径方向外側に供給さ
れるが、その訳は羽根によってこの区域に給送される液
体がその区域を分散区域とするからであり;また噴射リ
ングを使用することができる。The fluid is of course supplied radially outside the volume swept by the vanes, since the liquid delivered to this area by the vanes makes that area a dispersion area; also by using a spray ring. be able to.
さもなければ、ロータは貯槽に取付けられた噴射装置に
対して横方向にそしてその上方または下方に半径方向に
離して取付けることができ、また本質的に重力により供
給することが可能となる。Otherwise, the rotor can be mounted transversely to and radially spaced above or below the reservoir-mounted injector and can be essentially gravity fed.
噴射装置はロータ構造に従って、軸方向に一列に、横方
向に真直ぐにまたは弧状にもしくは平坦なあるいは湾曲
した格子状とするのが適当である。Depending on the rotor configuration, the injectors are suitably axially aligned, transversely straight or arcuate or in the form of a flat or curved grid.
別の態様において噴射装置はロータに、例えばそれぞれ
の羽根の前方のまたは前記または一つの羽根の平面から
軸方向に離れた孔(単数または複数)として、設けるこ
とができる。In another embodiment, the injector can be provided in the rotor, for example as a hole(s) in front of each blade or axially remote from the plane of said or one blade.
噴射装置および羽根の配置に適当したまたは匹敵するロ
ータの配置は熟練者にとって自明である。A suitable or comparable rotor arrangement to the injector and vane arrangement will be obvious to those skilled in the art.
本発明の集合体は、二つの流体相の分散が必要なすべで
の場合に有用であるが、とくに例えば生存細胞醗酵懸濁
物またはポリマ格子もしくは容易に減成もしくは凝固す
る分散物質のような敏感な層の、ガス−液体質量移送工
程に対し、低剪断完全混合用にとくに有用である。The assemblies of the invention are useful wherever dispersion of two fluid phases is required, but especially in live cell fermentation suspensions or polymer lattices or dispersed materials that degrade or solidify easily. It is particularly useful for low shear thorough mixing for gas-liquid mass transfer processes in sensitive layers.
以下、本発明を図面を参照して説明する。Hereinafter, the present invention will be explained with reference to the drawings.
図面において、ロータ4は(図示しない)貯槽2内に回
転可能に垂直に取付けられ貯槽2はロータ4が浸漬する
(同様に図示しない)液体3を保持している。ロータ4
は(図示しない電動機6によって駆動される)軸5を備
え、軸5には半径方向に延びる多数(4枚または6枚)
の羽根7が円板または腕8によって単一平面内に取付け
られている。In the drawing, the rotor 4 is rotatably mounted vertically in a reservoir 2 (not shown) which holds a liquid 3 (also not shown) in which the rotor 4 is immersed. Rotor 4
is equipped with a shaft 5 (driven by an electric motor 6, not shown), and the shaft 5 has a large number (4 or 6) of radially extending shafts.
vanes 7 are mounted in a single plane by disks or arms 8.
各羽根7は、羽根7の長手方向に延びる単一のくさび状
鋭角端部9を備えた均一な対称的大型断面のものである
。各羽根7は中空で、その先端面10は羽根7の長手方
向に延びる対称的に設けられたallを有する。羽根7
の端部12は開放している。羽根7はそれらの対称の中
心面が同−平面上にあるように取付けられている。Each vane 7 is of uniform, symmetrical, large cross-section with a single wedge-shaped sharp edge 9 extending in the longitudinal direction of the vane. Each vane 7 is hollow and its distal end surface 10 has a symmetrically disposed all extending in the longitudinal direction of the vane 7. Feather 7
The end 12 of is open. The vanes 7 are mounted so that their central planes of symmetry lie on the same plane.
ガスを噴出する装置14が、第1図ないし第3図に示す
ように、ロータの下方にかつそれと同軸に貯槽内に取付
けられている。第1図および第2図において、羽根7と
重ならない単一の孔または孔の噴射リングが示されてい
る。第3図において、噴射リングは使用中羽根が掃過す
る容積18の半径方向外側の区域19の下方にある。第
4図において、噴射装置14は中空軸5に取付けられ、
それから突出しかつその内部と連通し、そして羽根6の
間にかつそれと同一平面内に規則的に拡がった、4木の
有孔管より成っている。それらの孔15はそれぞれ管1
4の後端面16にある。A device 14 for ejecting gas is mounted in the reservoir below and coaxially with the rotor, as shown in FIGS. 1-3. In FIGS. 1 and 2, a single hole or hole injection ring that does not overlap the vanes 7 is shown. In FIG. 3, the injection ring is below the radially outer area 19 of the volume 18 that the vanes sweep during use. In FIG. 4, the injection device 14 is attached to the hollow shaft 5,
It consists of four perforated tubes projecting from it and communicating with its interior, and extending regularly between and in the same plane as the vanes 6. Those holes 15 are respectively connected to the tube 1
It is located on the rear end surface 16 of 4.
使用中、貯槽2は液体3を充填されロータ4の羽根7を
浸漬し、ロータ4は矢印Aの方向に回転される。ガス1
7は噴出孔15を通って(第4図においてはロータ軸5
およびロッド13の中空内部を通って)羽根が掃過する
容積18または区域19に供給される。すべての場合液
体3は溝11を通って羽根7にすくい上げられそして開
放した羽根の端部12を通って1分散区域19に排出さ
れる。第1図、第2図および第4図において、ガス17
は羽根7の外面上を流過しすべての場合ガスは区域19
内に分散される。In use, the reservoir 2 is filled with liquid 3 and immerses the blades 7 of the rotor 4, which is rotated in the direction of arrow A. gas 1
7 passes through the jet hole 15 (in Fig. 4, the rotor shaft 5
and through the hollow interior of the rod 13) into the volume 18 or area 19 that the vanes sweep. In all cases the liquid 3 is scooped up into the vane 7 through the groove 11 and discharged through the open vane end 12 into one dispersion area 19 . In FIGS. 1, 2 and 4, gas 17
flows over the outer surface of vane 7 and in all cases the gas passes through area 19
distributed within.
第1図、第2図、第3図および第4図は、ロータおよび
分散装置より成る本発明の四つの実施例の略図。
4−m−ロータ、5−・軸、7− 羽根、8−−一一一
円板(腕)9−(羽根の)後端、 10−(羽根の)先
端、 11− 溝。
12−−−(羽根の)端部、 13− ロッド、 1
4− 噴射管。1, 2, 3 and 4 are schematic illustrations of four embodiments of the invention comprising a rotor and a dispersion device. 4-m-rotor, 5--shaft, 7-blade, 8--111 disk (arm), 9-rear end (of the blade), 10-tip (of the blade), 11-groove. 12--end (of the vane), 13- rod, 1
4- Injection tube.
Claims (1)
びる羽根を有するロータ、および流体を貯槽内の液体中
に噴射する装置を備え、流体噴射装置およびロータは、
使用中、液体中に浸漬したロータ羽根およびロータ羽根
が発生した液体流のいずれか一方または双方が噴射され
た液体を分散するように構成配置されたタービン式攪拌
機集合体であつて、各羽根が中空でかつ不連続な端部、
鋭角をなす唯一つの後端部を有し、外側に凹状面を有せ
ずまた半径方向外端が開放していることを特徴とする、
タービン式攪拌機集合体。 2、各羽根がパラボラ状または楕円形状の先端断面から
くさび状後端部に滑らかに移行する対称的翼型断面を有
する、特許請求の範囲第1項に記載のタービン式攪拌機
集合体。 3、先端面に対称的に設けられた溝を有する特許請求の
範囲第2項に記載のタービン式攪拌機集合体。 4、羽根の面が羽根の回転面と一致するかそれに平行に
設けられた特許請求の範囲第2項に記載のタービン式攪
拌機集合体。 5、羽根が同一回転面内にまたは多数の平行な回転面内
に規則的に設けられた特許請求の範囲第1項に記載のタ
ービン式攪拌機集合体。 6、羽根が多数の平行な回転面内に設けられ各回転面は
同数の羽根を有し異なつた平面における対応する羽根が
軸方向に整合するかまたはすべての平面において回転方
向に規則的にずれている特許請求の範囲第5項に記載の
タービン式攪拌機集合体。 7、一つの回転面内に4枚ないし12枚の羽根を有する
特許請求の範囲第5項に記載のタービン式攪拌機集合体
。 8、羽根が水平な回転板に取付けられ集合体は使用中円
板が噴射された流体を羽根が掃過した容積に向けて偏向
するように設けられた特許請求の範囲第1項に記載の集
合体。 9、噴射装置は使用中噴射装置が噴射した流体を羽根が
掃過した容積の半径方向外側の区域に供給するように設
けられた特許請求の範囲第1項に記載の集合体。 10、噴射装置がロータに取付けられている特許請求の
範囲第1項に記載の集合体。[Claims] 1. A liquid storage tank, a rotor provided in the storage tank and having a large number of radially extending blades, and a device for injecting fluid into the liquid in the storage tank, the fluid injection device and the rotor comprising:
A turbine-type agitator assembly constructed and arranged such that, in use, either or both of the rotor blades immersed in the liquid and the liquid stream generated by the rotor blades disperses the injected liquid, the blades each being hollow and discontinuous ends;
characterized by having a single acutely angled rear end, having no external concave surface and being open at the radially outer end;
Turbine stirrer assembly. 2. The turbine-type agitator assembly according to claim 1, wherein each blade has a symmetrical airfoil cross-section that smoothly transitions from a parabolic or elliptical tip cross-section to a wedge-shaped rear end. 3. The turbine type agitator assembly according to claim 2, which has grooves symmetrically provided on the tip surface. 4. The turbine type agitator assembly according to claim 2, wherein the surface of the blade coincides with or is provided parallel to the rotational surface of the blade. 5. The turbine type agitator assembly according to claim 1, wherein the blades are regularly provided within the same rotation plane or within a plurality of parallel rotation planes. 6. The blades are arranged in a number of parallel planes of rotation, each plane of rotation having the same number of blades, and corresponding blades in different planes being aligned in the axial direction or regularly staggered in the direction of rotation in all planes. A turbine type agitator assembly according to claim 5. 7. The turbine type agitator assembly according to claim 5, which has 4 to 12 blades in one rotational plane. 8. The vane is mounted on a horizontal rotating plate and the assembly is arranged such that in use the disc deflects the injected fluid towards the volume swept by the vane. Aggregation. 9. An assembly according to claim 1, wherein the injector is arranged such that, in use, the injector supplies the fluid injected by the injector to an area radially outside the volume swept by the vanes. 10. The assembly according to claim 1, wherein the injection device is attached to the rotor.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8603904 | 1986-02-17 | ||
GB868603904A GB8603904D0 (en) | 1986-02-17 | 1986-02-17 | Agitators |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62193635A true JPS62193635A (en) | 1987-08-25 |
Family
ID=10593203
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62032568A Pending JPS62193635A (en) | 1986-02-17 | 1987-02-17 | Turbine type stirrer assembly |
Country Status (12)
Country | Link |
---|---|
EP (1) | EP0234768B1 (en) |
JP (1) | JPS62193635A (en) |
AT (1) | ATE83169T1 (en) |
AU (1) | AU580702B2 (en) |
CA (1) | CA1257196A (en) |
DE (1) | DE3782951T2 (en) |
ES (1) | ES2037078T3 (en) |
GB (1) | GB8603904D0 (en) |
HK (1) | HK1001041A1 (en) |
IE (1) | IE60597B1 (en) |
NZ (1) | NZ219280A (en) |
ZA (1) | ZA87882B (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003010664A (en) * | 2001-07-03 | 2003-01-14 | Kawata Mfg Co Ltd | Mixing device for powdery/granular material |
JP2014136203A (en) * | 2013-01-18 | 2014-07-28 | Chugoku Electric Power Co Inc:The | Agitator |
JP2015502846A (en) * | 2011-11-24 | 2015-01-29 | ワン、リーWANG, Li | Stirring impeller with channel blades |
JP2015078439A (en) * | 2014-11-20 | 2015-04-23 | グローバルアドバンストメタルジャパン株式会社 | Method of producing nitrogen-containing metal powder |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0441505A1 (en) * | 1990-02-05 | 1991-08-14 | Imperial Chemical Industries Plc | Agitators |
GB2268420B (en) * | 1992-07-04 | 1995-11-29 | Flow Research Evaluation Diagn | Improvements relating to liquid treatment apparatus |
US5791780A (en) * | 1997-04-30 | 1998-08-11 | Chemineer, Inc. | Impeller assembly with asymmetric concave blades |
DE10336054B4 (en) * | 2003-08-01 | 2005-12-15 | Domo Caproleuna Gmbh | Process for the preparation of hydroxylammonium salts |
DE102007001711A1 (en) * | 2007-01-11 | 2008-07-17 | EKATO Rühr- und Mischtechnik GmbH | Stirring arrangement with a stirrer and a gassing device |
US20080199321A1 (en) * | 2007-02-16 | 2008-08-21 | Spx Corporation | Parabolic radial flow impeller with tilted or offset blades |
NL2009286C2 (en) * | 2012-08-06 | 2014-02-10 | Stichting Energie | Swallow tail airfoil. |
US11136958B2 (en) | 2012-08-06 | 2021-10-05 | Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno | Swallow tail airfoil |
CN102974504B (en) * | 2012-12-06 | 2016-05-18 | 济南圣泉集团股份有限公司 | A kind of anti-precipitation coating machine |
DE102013002060A1 (en) * | 2013-02-07 | 2014-08-07 | Wilfried Rummel | Apparatus for producing colloidal fluids with a colloidation vessel and method |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5724624A (en) * | 1980-07-18 | 1982-02-09 | Shozo Urashi | Vapor-liquid contact apparatus |
JPS5759625A (en) * | 1980-09-29 | 1982-04-10 | Yoichi Nagase | Stirring blade |
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DE2207144A1 (en) * | 1972-02-16 | 1973-08-30 | Schoeller Bleckmann Stahlwerke | Liquid aerating appts - using vanes with determined gas exit width to vane width ratio |
AU502018B2 (en) * | 1976-05-04 | 1979-07-12 | United States Filter Corporation | Mixing apparatus |
US4159181A (en) * | 1976-12-23 | 1979-06-26 | American Pelletizing Corporation | Mixing and pelletizing machine |
AU509477B2 (en) * | 1977-09-05 | 1980-05-15 | Gousti International Ltd. | Mixing apparatus |
US4305673A (en) * | 1980-03-25 | 1981-12-15 | General Signal Corporation | High efficiency mixing impeller |
SE461444B (en) * | 1985-11-21 | 1990-02-19 | Boerje Skaanberg | IMPELLER APPLIED FOR THE STIRRING OF FLUID DURING DISPERSION OF GAS THEREOF |
-
1986
- 1986-02-17 GB GB868603904A patent/GB8603904D0/en active Pending
-
1987
- 1987-02-02 EP EP87300911A patent/EP0234768B1/en not_active Expired - Lifetime
- 1987-02-02 DE DE8787300911T patent/DE3782951T2/en not_active Expired - Lifetime
- 1987-02-02 AT AT87300911T patent/ATE83169T1/en not_active IP Right Cessation
- 1987-02-02 ES ES198787300911T patent/ES2037078T3/en not_active Expired - Lifetime
- 1987-02-03 IE IE27987A patent/IE60597B1/en not_active IP Right Cessation
- 1987-02-06 ZA ZA87882A patent/ZA87882B/en unknown
- 1987-02-10 CA CA000529394A patent/CA1257196A/en not_active Expired
- 1987-02-13 AU AU68764/87A patent/AU580702B2/en not_active Ceased
- 1987-02-16 NZ NZ219280A patent/NZ219280A/en unknown
- 1987-02-17 JP JP62032568A patent/JPS62193635A/en active Pending
-
1997
- 1997-12-09 HK HK97102369A patent/HK1001041A1/en not_active IP Right Cessation
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5724624A (en) * | 1980-07-18 | 1982-02-09 | Shozo Urashi | Vapor-liquid contact apparatus |
JPS5759625A (en) * | 1980-09-29 | 1982-04-10 | Yoichi Nagase | Stirring blade |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003010664A (en) * | 2001-07-03 | 2003-01-14 | Kawata Mfg Co Ltd | Mixing device for powdery/granular material |
JP2015502846A (en) * | 2011-11-24 | 2015-01-29 | ワン、リーWANG, Li | Stirring impeller with channel blades |
JP2014136203A (en) * | 2013-01-18 | 2014-07-28 | Chugoku Electric Power Co Inc:The | Agitator |
JP2015078439A (en) * | 2014-11-20 | 2015-04-23 | グローバルアドバンストメタルジャパン株式会社 | Method of producing nitrogen-containing metal powder |
Also Published As
Publication number | Publication date |
---|---|
ZA87882B (en) | 1987-10-28 |
ES2037078T3 (en) | 1993-06-16 |
GB8603904D0 (en) | 1986-03-26 |
DE3782951D1 (en) | 1993-01-21 |
IE60597B1 (en) | 1994-07-27 |
IE870279L (en) | 1987-08-17 |
AU580702B2 (en) | 1989-01-27 |
EP0234768A3 (en) | 1989-04-26 |
EP0234768B1 (en) | 1992-12-09 |
EP0234768A2 (en) | 1987-09-02 |
NZ219280A (en) | 1988-10-28 |
AU6876487A (en) | 1987-08-20 |
CA1257196A (en) | 1989-07-11 |
DE3782951T2 (en) | 1993-07-08 |
ATE83169T1 (en) | 1992-12-15 |
HK1001041A1 (en) | 1998-05-22 |
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